EP1070022B1 - A device for the treatment of water - Google Patents

A device for the treatment of water Download PDF

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Publication number
EP1070022B1
EP1070022B1 EP99911639A EP99911639A EP1070022B1 EP 1070022 B1 EP1070022 B1 EP 1070022B1 EP 99911639 A EP99911639 A EP 99911639A EP 99911639 A EP99911639 A EP 99911639A EP 1070022 B1 EP1070022 B1 EP 1070022B1
Authority
EP
European Patent Office
Prior art keywords
drops
layers
water
pipe
wire
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
EP99911639A
Other languages
German (de)
French (fr)
Other versions
EP1070022A1 (en
Inventor
Finn Lebech
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Unicon Beton Holding AS
Original Assignee
Unicon Beton Holding AS
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Unicon Beton Holding AS filed Critical Unicon Beton Holding AS
Publication of EP1070022A1 publication Critical patent/EP1070022A1/en
Application granted granted Critical
Publication of EP1070022B1 publication Critical patent/EP1070022B1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/04Aerobic processes using trickle filters
    • C02F3/043Devices for distributing water over trickle filters
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/74Treatment of water, waste water, or sewage by oxidation with air
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/04Aerobic processes using trickle filters
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Definitions

  • the crude water is aerated according to the prior art to add to the water a greater content of oxygen which contributes to the conversion of iron and manganese bicarbonate into sparingly soluble compounds, ferrous hydroxide and pyrolusite and causes separation of CO 2 , hydrogen sulphide and methane.
  • the aeration takes place e.g. in that the water is introduced over a perforated tray and drops freely from there as drops toward a basin, or in that the water flows down over oxidation steps.
  • the object of the present invention is to provide an apparatus by means of which crude water may be treated to achieve a satisfactory water quality with respect to content of components which can be removed or at least reduced by aeration.
  • drops are initially formed from an introduced water amount and the formed drops are divided by mechanical action to form microdrops.
  • Such a formation of microdrops results in a considerably larger surface of the drops relative to the volume of the drops, and improved oxidation can thus take place.
  • the mechanical action ensures that the intended division takes place. It has been found that a division of 50-60 times or optionally more causes formation of drops of a size which is sufficiently small for a satisfactory oxidation to take place, and thereby for a satisfactory water quality to be obtained.
  • a microorganism culture may additionally be added to the water prior to the initiating drop formation.
  • components of the crude water which are not converted by the oxidation alone may moreover be removed or reduced by the metabolism of the microorganisms.
  • the concrete microorganism culture may be selected depending on the crude water content of components whose amount is to be reduced.
  • the formed microdrops are introduced into a sedimentation container after completed oxidation. After settling in such a container the water may be conveyed to the user.
  • the apparatus of the invention comprises a plate with holes for forming drops by the flow of the water through these holes at the initiation of the process, and, in the direction of the gravitational force below these means, additional means for causing division of the drops by contact with these.
  • the means for causing division of the drops comprise wire-shaped elements mutually spaced in the direction of the gravitational force.
  • the wire-shaped elements are hereby arranged in a mutually intersecting pattern.
  • Such a structure involves a good certainty of drop division, and it has moreover been found by tests that good environmental conditions are hereby formed for an optionally added microorganism culture.
  • At least 50-60 layers of the mutually spaced wire-shaped elements are preferably arranged in the direction of the gravitational force to obtain an expedient fine division of the drops, as described above.
  • more of these layers are arranged so that also the drops which statistically drop through a layer in a gap between two wire-shaped elements, will obtain a division of 50-60 times.
  • the mutual spacing between parallel or substantially parallel wire-shaped elements in the same layer is expediently between 5 and 15 mm, preferably about 10 mm.
  • the spacing between the wires in the same layer will affect the statistical fall of drops, which are thus not divided as there is no contact. A too small spacing between the wires may cause gathering of already divided drops.
  • the mutual spacing between the layers of wire-shaped elements is preferably 30-60 mm, and more preferably 40-50 mm. This ensures that sufficient kinetic energy is added to the drops for rotation to take place, while ensuring that a complete system still has a limited height.
  • means are arranged in the apparatus for collecting the microdrops below the means for dividing the drops.
  • the drops or the caught drops, which form an amount of water, are expediently introduced into a settling container, which forms part of the apparatus in this connection.
  • Fig. 1 illustrates a system which uses apparatuses according to the invention for performing the method according to the invention.
  • a system comprises a pipe connection 1 from a bore well and a pump 2 for pumping the water from the bore well.
  • the crude water is conveyed via the pipe 1 to a distribution system consisting of a plate 3 with holes 4.
  • This plate 3 with holes 4 serves to initiate formation of drops. Relatively large drops are involved in this connection.
  • the drops leaving the plate 3 through the holes 4 in it then fall down under the action of gravity and hereby contact rows of wire-shaped elements, which, in the example shown, are formed by tubular elements 5, 6 arranged side by side with horizontal pipe axes to form pipe layers, a plurality of such pipe layers being arranged on top of each other.
  • the pipe layers are arranged such that every second pipe layer 6 is rotated 90°. In the structure shown, 15 pipe layers are provided. In this constellation, in the event that a large content of components is to be reduced, it will be necessary to recirculate the water to achieve sufficient oxidation. As also mentioned in the preamble to the description, 30-40 pipe layers will expediently be provided.
  • the pipe layers are arranged in a housing 7 which is open at the top and at the bottom. When the water drops leave the lowermost pipe layer at the lower end of the housing 7, the water is collected in a collection basin or a settling container 8, in which solids, if any, can precipitate, and from which the cleaned water may be discharged and transported to the place of use.
  • Fig. 2 shows the plate 3 more clearly seen from above.
  • the holes 4 have a diameter of about 1-2 mm. This diameter may be selected depending on the surface tension of the water, the water pressure, etc.
  • Fig. 3 shows a pipe element which is used for the construction of the pipe layers in the housing.
  • the pipe layers are composed of wire-shaped elements 9 which are arranged in intersecting manner in the pipe wall. By their mutually intersecting pattern, the wire-shaped elements 9 form rhomboid holes in the pipe wall.
  • Fig. 4 shows four such pipe elements in an interconnected state. It appears that circular pipe elements 5 are involved.

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Microbiology (AREA)
  • Physical Water Treatments (AREA)
  • Biological Treatment Of Waste Water (AREA)
  • Removal Of Specific Substances (AREA)
  • Excavating Of Shafts Or Tunnels (AREA)
  • Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)
  • Water Treatment By Sorption (AREA)

Abstract

The invention relates to treatment of water, comprising initiating formation of drops from an introduced amount of water and division of the formed drops to form microdrops preferably by division at least 50-60 times. The invention also relates to an apparatus for performing the invention.

Description

In connection with the treatment of water, the crude water is aerated according to the prior art to add to the water a greater content of oxygen which contributes to the conversion of iron and manganese bicarbonate into sparingly soluble compounds, ferrous hydroxide and pyrolusite and causes separation of CO2, hydrogen sulphide and methane. According to the prior art, the aeration takes place e.g. in that the water is introduced over a perforated tray and drops freely from there as drops toward a basin, or in that the water flows down over oxidation steps.
These known methods have some effect on the water in respect of achieving the intended result, as described above. However, in many cases this treatment is not sufficient. In many cases the insufficiency is caused by an ever poorer crude water quality with a larger content of harmful substances, which must be removed, e.g. by aeration.
Accordingly, the object of the present invention is to provide an apparatus by means of which crude water may be treated to achieve a satisfactory water quality with respect to content of components which can be removed or at least reduced by aeration.
According to the invention, drops are initially formed from an introduced water amount and the formed drops are divided by mechanical action to form microdrops.
Such a formation of microdrops results in a considerably larger surface of the drops relative to the volume of the drops, and improved oxidation can thus take place. The mechanical action ensures that the intended division takes place. It has been found that a division of 50-60 times or optionally more causes formation of drops of a size which is sufficiently small for a satisfactory oxidation to take place, and thereby for a satisfactory water quality to be obtained.
According to an expedient embodiment, a microorganism culture may additionally be added to the water prior to the initiating drop formation. Hereby, components of the crude water which are not converted by the oxidation alone, may moreover be removed or reduced by the metabolism of the microorganisms. In this connection, the concrete microorganism culture may be selected depending on the crude water content of components whose amount is to be reduced.
Particularly expediently, the formed microdrops are introduced into a sedimentation container after completed oxidation. After settling in such a container the water may be conveyed to the user.
The apparatus of the invention comprises a plate with holes for forming drops by the flow of the water through these holes at the initiation of the process, and, in the direction of the gravitational force below these means, additional means for causing division of the drops by contact with these.
The means for causing division of the drops comprise wire-shaped elements mutually spaced in the direction of the gravitational force. The wire-shaped elements are hereby arranged in a mutually intersecting pattern. Such a structure involves a good certainty of drop division, and it has moreover been found by tests that good environmental conditions are hereby formed for an optionally added microorganism culture. At least 50-60 layers of the mutually spaced wire-shaped elements are preferably arranged in the direction of the gravitational force to obtain an expedient fine division of the drops, as described above. Preferably, however, more of these layers are arranged so that also the drops which statistically drop through a layer in a gap between two wire-shaped elements, will obtain a division of 50-60 times. Thus, 70-80 layers of wire-shaped elements are expediently arranged. In this connection, the mutual spacing between parallel or substantially parallel wire-shaped elements in the same layer is expediently between 5 and 15 mm, preferably about 10 mm. The spacing between the wires in the same layer will affect the statistical fall of drops, which are thus not divided as there is no contact. A too small spacing between the wires may cause gathering of already divided drops.
The mutual spacing between the layers of wire-shaped elements is preferably 30-60 mm, and more preferably 40-50 mm. This ensures that sufficient kinetic energy is added to the drops for rotation to take place, while ensuring that a complete system still has a limited height.
It has been found expedient to build such a system of tubular elements with an interlaced structure. In this connection, a row of such pipes are placed side by side to form a pipe layer. A plurality of such pipe layers are stacked to form a pipe column. Each pipe layer thus forms two layers of wire-shaped elements mutually spaced, except in the pipe areas adjoining each other in the same layer. In this connection, the pipe layers are expediently arranged with the pipe axes rotated 90 degrees relative to overlying and underlying pipe layers. This has been found to give a particularly good result, and at the same time an increased mechanical stability is achieved.
Preferably, means are arranged in the apparatus for collecting the microdrops below the means for dividing the drops. The drops or the caught drops, which form an amount of water, are expediently introduced into a settling container, which forms part of the apparatus in this connection.
The invention will be explained more fully below with reference to the drawing, in which a preferred embodiment of the invention is shown schematically, and in which
  • fig. 1 shows an apparatus, seen from the side,
  • fig. 2 shows an apparatus, seen from above, and
  • fig. 3 shows a pipe element associated with the apparatus shown in figs. 1 and 2, and
  • fig. 4 shows four interconnected pipe elements, as shown in fig. 3 and seen from the end.
  • Fig. 1 illustrates a system which uses apparatuses according to the invention for performing the method according to the invention. Such a system comprises a pipe connection 1 from a bore well and a pump 2 for pumping the water from the bore well. The crude water is conveyed via the pipe 1 to a distribution system consisting of a plate 3 with holes 4. This plate 3 with holes 4 serves to initiate formation of drops. Relatively large drops are involved in this connection. The drops leaving the plate 3 through the holes 4 in it then fall down under the action of gravity and hereby contact rows of wire-shaped elements, which, in the example shown, are formed by tubular elements 5, 6 arranged side by side with horizontal pipe axes to form pipe layers, a plurality of such pipe layers being arranged on top of each other. The pipe layers are arranged such that every second pipe layer 6 is rotated 90°. In the structure shown, 15 pipe layers are provided. In this constellation, in the event that a large content of components is to be reduced, it will be necessary to recirculate the water to achieve sufficient oxidation. As also mentioned in the preamble to the description, 30-40 pipe layers will expediently be provided. The pipe layers are arranged in a housing 7 which is open at the top and at the bottom. When the water drops leave the lowermost pipe layer at the lower end of the housing 7, the water is collected in a collection basin or a settling container 8, in which solids, if any, can precipitate, and from which the cleaned water may be discharged and transported to the place of use.
    Fig. 2 shows the plate 3 more clearly seen from above. In this connection, the holes 4 have a diameter of about 1-2 mm. This diameter may be selected depending on the surface tension of the water, the water pressure, etc.
    Fig. 3 shows a pipe element which is used for the construction of the pipe layers in the housing. The pipe layers are composed of wire-shaped elements 9 which are arranged in intersecting manner in the pipe wall. By their mutually intersecting pattern, the wire-shaped elements 9 form rhomboid holes in the pipe wall. Fig. 4 shows four such pipe elements in an interconnected state. It appears that circular pipe elements 5 are involved.

    Claims (7)

    1. An apparatus for treatment of water comprising:
      a plate (3) formed with holes for forming drops by flow of the water through the holes at the initiation of the treatment process, and
      means (5,6) arranged below said plate (3) for causing division of the drops by contact therewith,
      characterized in that the means for causing division of the drops comprise layers of mutually intersecting wire-shaped element (5,6), said layers being mutually spaced in the direction of the gravitational force, said mutually intersecting wire-shaped elements being arranged so as to form tubular elements (5,6), a plurality of said tubular elements being arranged horizontally side by side and on top of each other.
    2. An apparatus according to claim 1, characterized in that in every second layer (6) the tubular elements (6) extend in a direction perpendicular to the orientation of the tubular elements of adjacent layers.
    3. An apparatus according to claims 1 or 2, characterized in that at least 50-60 layers of mutually spaced layers of mutually intersecting wire-shaped elements are arranged in the direction of gravitational force.
    4. An apparatus according to claims 1, 2 or 3, characterized in that the mutual spacing between the layers of wire-shaped elements is 30-60 mm, preferably 40-50 mm.
    5. An apparatus according to any of claims 1-4, characterized in that means are provided for collecting the microdrops below the means for dividing the drops.
    6. An apparatus according to any of claims 1-5, characterized by comprising a settling container.
    7. The use of an apparatus according to any of claims 1-6, characterized in that a microorganism culture is added to the water prior to the initiating drop formation.
    EP99911639A 1998-04-01 1999-03-30 A device for the treatment of water Expired - Lifetime EP1070022B1 (en)

    Applications Claiming Priority (3)

    Application Number Priority Date Filing Date Title
    DK45998 1998-04-01
    DK45998 1998-04-01
    PCT/DK1999/000186 WO1999052829A1 (en) 1998-04-01 1999-03-30 A method and a device for the treatment of water

    Publications (2)

    Publication Number Publication Date
    EP1070022A1 EP1070022A1 (en) 2001-01-24
    EP1070022B1 true EP1070022B1 (en) 2002-11-13

    Family

    ID=8093797

    Family Applications (1)

    Application Number Title Priority Date Filing Date
    EP99911639A Expired - Lifetime EP1070022B1 (en) 1998-04-01 1999-03-30 A device for the treatment of water

    Country Status (8)

    Country Link
    EP (1) EP1070022B1 (en)
    AT (1) ATE227696T1 (en)
    AU (1) AU3025499A (en)
    DE (1) DE69903931T2 (en)
    DK (1) DK1070022T3 (en)
    ES (1) ES2188144T3 (en)
    PT (1) PT1070022E (en)
    WO (1) WO1999052829A1 (en)

    Families Citing this family (4)

    * Cited by examiner, † Cited by third party
    Publication number Priority date Publication date Assignee Title
    DK200500694A (en) * 2005-05-12 2006-11-13 Microdrop Aqua Aps Process and plant for removing pollutants, especially arsenic, from water
    DK201170014A (en) * 2011-01-11 2012-07-12 Microdrop Aqua Aps A method for preparing potable water from contaminated crude water
    CN103946162B (en) * 2011-09-23 2016-04-20 微滴爱克有限责任公司 For blowing down the method and apparatus of gaseous pollutant in tap water production from former water
    EP3342284B1 (en) * 2016-12-29 2022-01-26 NP Innovation AB Aerator and carbon dioxide separator

    Family Cites Families (4)

    * Cited by examiner, † Cited by third party
    Publication number Priority date Publication date Assignee Title
    US4562015A (en) * 1984-05-22 1985-12-31 The Munters Corporation Open mesh fill assembly
    AT391753B (en) * 1987-06-02 1990-11-26 Foidl Leonhard AIR HUMIDIFICATION DEVICE
    GB2241697B (en) * 1989-12-06 1993-04-14 D L Herbertson Limited Modular aeration unit
    DK168684B1 (en) * 1993-08-06 1994-05-24 Nielsen Hede As Reactor for oxygen enrichment of fluid - has upright reactor at top of which fluid is inserted through inlet with one or more openings, and gas contg. oxygen inserted through reactor base from which oxygen-enriched fluid is withdrawn

    Also Published As

    Publication number Publication date
    DE69903931T2 (en) 2003-07-31
    DK1070022T3 (en) 2003-03-10
    EP1070022A1 (en) 2001-01-24
    ES2188144T3 (en) 2003-06-16
    PT1070022E (en) 2003-03-31
    DE69903931D1 (en) 2002-12-19
    ATE227696T1 (en) 2002-11-15
    AU3025499A (en) 1999-11-01
    WO1999052829A1 (en) 1999-10-21

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